JPH11130723A - Dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid compound or dianhydride thereof and method for producing the same - Google Patents
Dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid compound or dianhydride thereof and method for producing the sameInfo
- Publication number
- JPH11130723A JPH11130723A JP9292328A JP29232897A JPH11130723A JP H11130723 A JPH11130723 A JP H11130723A JP 9292328 A JP9292328 A JP 9292328A JP 29232897 A JP29232897 A JP 29232897A JP H11130723 A JPH11130723 A JP H11130723A
- Authority
- JP
- Japan
- Prior art keywords
- dicyclohexyl
- tetracarboxylic acid
- dianhydride
- acid compound
- ester
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 8
- -1 tetracarboxylic acid compound Chemical class 0.000 claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims description 21
- 238000005984 hydrogenation reaction Methods 0.000 claims description 15
- 238000006297 dehydration reaction Methods 0.000 claims description 7
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 229910000510 noble metal Inorganic materials 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 4
- 238000006460 hydrolysis reaction Methods 0.000 claims description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- 230000007062 hydrolysis Effects 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 2
- 239000002253 acid Substances 0.000 abstract description 7
- 150000001875 compounds Chemical class 0.000 abstract description 3
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 12
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 239000002904 solvent Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000013078 crystal Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000000862 absorption spectrum Methods 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 5
- 150000002148 esters Chemical class 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005160 1H NMR spectroscopy Methods 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 150000008064 anhydrides Chemical class 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052703 rhodium Inorganic materials 0.000 description 3
- 239000010948 rhodium Substances 0.000 description 3
- NBAUUNCGSMAPFM-UHFFFAOYSA-N 3-(3,4-dicarboxyphenyl)phthalic acid Chemical compound C1=C(C(O)=O)C(C(=O)O)=CC=C1C1=CC=CC(C(O)=O)=C1C(O)=O NBAUUNCGSMAPFM-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 125000005907 alkyl ester group Chemical group 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N o-dicarboxybenzene Natural products OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical group N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 description 1
- YRSUYCONXJDKKZ-UHFFFAOYSA-N COC(=O)C1=C(C=CC=C1C(=O)O)C1=CC(=C(C=C1)C(=O)O)C(=O)O Chemical class COC(=O)C1=C(C=CC=C1C(=O)O)C1=CC(=C(C=C1)C(=O)O)C(=O)O YRSUYCONXJDKKZ-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- OJURWUUOVGOHJZ-UHFFFAOYSA-N methyl 2-[(2-acetyloxyphenyl)methyl-[2-[(2-acetyloxyphenyl)methyl-(2-methoxy-2-oxoethyl)amino]ethyl]amino]acetate Chemical compound C=1C=CC=C(OC(C)=O)C=1CN(CC(=O)OC)CCN(CC(=O)OC)CC1=CC=CC=C1OC(C)=O OJURWUUOVGOHJZ-UHFFFAOYSA-N 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002940 palladium Chemical class 0.000 description 1
- YJVFFLUZDVXJQI-UHFFFAOYSA-L palladium(ii) acetate Chemical compound [Pd+2].CC([O-])=O.CC([O-])=O YJVFFLUZDVXJQI-UHFFFAOYSA-L 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 125000006158 tetracarboxylic acid group Chemical group 0.000 description 1
- 229940045860 white wax Drugs 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Furan Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
(57)【要約】
【課題】 新規なジシクロヘキシルテトラカルボン酸化
合物又はその二無水物およびその製造法を提供する。
【解決手段】 シクロヘキシル−2,3,3’,4’−
テトラカルボン酸化合物、その二無水物およびビフェニ
ル−2,3,3’,4’−テトラカルボン酸エステルを
水素化する工程を含むシクロヘキシル−2,3,3’,
4’−テトラカルボン酸化合物又はその二無水物の製造
法に関する。
(57) [Problem] To provide a novel dicyclohexyltetracarboxylic acid compound or a dianhydride thereof and a method for producing the same. SOLUTION: Cyclohexyl-2,3,3 ', 4'-
Cyclohexyl-2,3,3 ′, comprising a step of hydrogenating a tetracarboxylic acid compound, its dianhydride and biphenyl-2,3,3 ′, 4′-tetracarboxylic acid ester.
The present invention relates to a method for producing a 4′-tetracarboxylic acid compound or a dianhydride thereof.
Description
【0001】[0001]
【発明の属する技術分野】この発明は、新規なジシクロ
ヘキシルテトラカルボン酸類化合物であるジシクロヘキ
シル−2,3,3’,4’−テトラカルボン酸、エステ
ル又はその二無水物およびその製造法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel dicyclohexyltetracarboxylic acid compound, dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid, ester or dianhydride thereof, and a method for producing the same. .
【0002】[0002]
【従来の技術】従来、工業的に製造されている芳香族テ
トラカルボン酸を水素化反応させたジシクロヘキシルテ
トラカルボン酸又はその二無水物としては、特開平1−
96147号公報に記載されているジシクロヘキシル−
3,3’,4,4’−テトラカルボン酸又はその二無水
物が知られているにすぎない。2. Description of the Related Art Conventionally, dicyclohexyltetracarboxylic acid obtained by hydrogenating an aromatic tetracarboxylic acid industrially produced or dianhydride thereof is disclosed in
Dicyclohexyl- described in JP-A-96147.
Only 3,3 ', 4,4'-tetracarboxylic acid or its dianhydride is known.
【0003】[0003]
【発明が解決しようとする課題】この発明の目的は、新
規なジシクロヘキシルテトラカルボン酸またはその二無
水物およびその製造法を提供することである。SUMMARY OF THE INVENTION An object of the present invention is to provide a novel dicyclohexyltetracarboxylic acid or a dianhydride thereof and a method for producing the same.
【0004】[0004]
【課題を解決するための手段】すなわち、この発明は、
下記一般式で表されるジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸化合物に関する。That is, the present invention provides:
Dicyclohexyl-2,3 represented by the following general formula
It relates to a 3 ', 4'-tetracarboxylic acid compound.
【化3】 (式中、Xは水素原子、又は炭素数1以上のアルキル基
を示す。) また、この発明は、下記一般式で表されるジシクロヘキ
シル−2,3,3’,4’−テトラカルボン酸二無水物
に関する。Embedded image (In the formula, X represents a hydrogen atom or an alkyl group having 1 or more carbon atoms.) Further, the present invention provides dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid represented by the following general formula: Related to anhydride.
【化4】 さらに、この発明は、ビフェニル−2,3,3’,4’
−テトラカルボン酸エステルを貴金属水素化触媒または
貴金属の坦持触媒などの水素化触媒によって水素化反応
させる工程を含み、必要であればさらに加水分解、無水
化処理する工程を含むジシクロヘキシル−2,2,
3’,4’−テトラカルボン酸化合物又はその二無水物
の製造法に関する。Embedded image Further, the present invention relates to biphenyl-2,3,3 ', 4'
Dicyclohexyl-2,2 comprising a step of hydrogenating the tetracarboxylic acid ester with a hydrogenation catalyst such as a noble metal hydrogenation catalyst or a noble metal supported catalyst, and further comprising a step of hydrolyzing and dehydrating if necessary. ,
The present invention relates to a method for producing a 3 ′, 4′-tetracarboxylic acid compound or a dianhydride thereof.
【0005】この発明のジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸化合物としては、ジシク
ロヘキシル−2,3,3’,4’−テトラカルボン酸、
ジシクロヘキシル−2,3,3’,4’−テトラカルボ
ン酸メチルエステル、ジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸エチルエステル、ジシク
ロヘキシル−2,3,3’,4’−テトラカルボン酸イ
ソプロピルエステル、ジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸n−ブチルエステルなど
を挙げることができる。[0005] The dicyclohexyl-2,3,
Examples of the 3 ′, 4′-tetracarboxylic acid compound include dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid,
Dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid methyl ester, dicyclohexyl-2,3,3
3 ′, 4′-tetracarboxylic acid ethyl ester, dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid isopropyl ester, dicyclohexyl-2,3
3 ', 4'-tetracarboxylic acid n-butyl ester and the like can be mentioned.
【0006】この発明において使用されるビフェニル−
2,3,3’,4’−テトラカルボン酸アルキルエステ
ルは公知の化合物であって、例えば特公昭60−333
79号公報、特公昭61−57821号公報に記載の方
法によって製造することができる。例えば、フタル酸ジ
エステルを酸素、パラジウム塩および1,10−フェナ
ンソロリンまたはビピリジルの触媒によって酸素存在
下、カップリング反応させた後、生成したビフェニル−
2,3,3’,4’−テトラカルボン酸メチルエステル
などのアルキルエステルを含む混合物から、触媒および
溶媒を除去した後、蒸留法によって得ることができる。
このビフェニル−2,3,3’,4’−テトラカルボン
酸メチルエステルは、沸点が200(1mmHg)℃、
融点が75℃の白色結晶である。The biphenyl used in the present invention
2,3,3 ', 4'-tetracarboxylic acid alkyl ester is a known compound, for example, JP-B-60-333.
No. 79 and Japanese Patent Publication No. 61-57821. For example, a phthalic acid diester is subjected to a coupling reaction in the presence of oxygen using a catalyst of oxygen, a palladium salt and 1,10-phenanthroline or bipyridyl, and then formed biphenyl-
After removing the catalyst and the solvent from a mixture containing an alkyl ester such as 2,3,3 ′, 4′-tetracarboxylic acid methyl ester, the mixture can be obtained by a distillation method.
This biphenyl-2,3,3 ′, 4′-tetracarboxylic acid methyl ester has a boiling point of 200 (1 mmHg) ° C.
It is a white crystal with a melting point of 75 ° C.
【0007】この発明のジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸化合物は、好適には次の
ようにして製造することができる。すなわち、前記のビ
フェニル−2,3,3’,4’−テトラカルボン酸エス
テルを溶媒に溶解させて水素化触媒の存在下水素化反応
を行わせる。使用する溶媒としては、ビフェニル−2,
3,3’,4’−テトラカルボン酸エステルを溶解し、
水素化反応時に副反応を生じない溶媒であればよく、メ
チルアルコ−ル、エチルアルコ−ルなどの炭素数1以上
の脂肪族アルコ−ル類、酢酸メチル、酢酸エチルなどの
炭素数3以上のエステル類、テトラヒドロフラン、ジメ
チルエ−テル、ジイソプロピルエ−テルなどの炭素数4
以上のエ−テル類、ノルマルヘキサン、シクロヘキサン
などの炭素数6以上の炭化水素類などが挙げられる。前
記の水素化触媒としては、金属ロジウム粉末、金属ルテ
ニウム粉末やこれらの金属を活性炭、アルミナ、珪藻
土、シリカ等の担体に担持させた触媒などが挙げられ
る。担持触媒の場合、貴金属換算で0.1−10重量%
の担持量であることが好ましい。前記の水素化触媒の使
用量は通常ビフェニル−2,3,3’,4’−テトラカ
ルボン酸エステルに対して、金属換算で2−50重量%
であることが好ましい。The dicyclohexyl-2,3 of the present invention
The 3 ′, 4′-tetracarboxylic acid compound can be preferably produced as follows. That is, the above-mentioned biphenyl-2,3,3 ', 4'-tetracarboxylic acid ester is dissolved in a solvent, and a hydrogenation reaction is performed in the presence of a hydrogenation catalyst. As a solvent to be used, biphenyl-2,
Dissolving 3,3 ′, 4′-tetracarboxylic acid ester,
Any solvent that does not cause a side reaction at the time of the hydrogenation reaction may be used, and aliphatic alcohols having 1 or more carbon atoms such as methyl alcohol and ethyl alcohol, and esters having 3 or more carbon atoms such as methyl acetate and ethyl acetate. , Tetrahydrofuran, dimethyl ether, diisopropyl ether and the like having 4 carbon atoms
The above-mentioned ethers, hydrocarbons having 6 or more carbon atoms such as normal hexane and cyclohexane are exemplified. Examples of the hydrogenation catalyst include a metal rhodium powder, a metal ruthenium powder, and a catalyst in which these metals are supported on a carrier such as activated carbon, alumina, diatomaceous earth, and silica. In the case of a supported catalyst, 0.1-10% by weight in terms of noble metal
Is preferably carried. The amount of the hydrogenation catalyst used is usually 2 to 50% by weight in terms of metal based on biphenyl-2,3,3 ', 4'-tetracarboxylic acid ester.
It is preferred that
【0008】前記の水素化反応を行わせる条件は、触媒
によって異なるが、通常水素圧力が数kg/cm2 −1
00kg/cm2 、特に20−50kg/cm2 であ
り、温度が20−200℃、特に50−150℃であ
り、反応時間が数10分−24時間程度であることが好
ましい。水素化反応の進行状態および終了に関しては、
圧力計から消費水素量を求めることによって判断するこ
とができる。反応が終了したら、反応混合物から濾過操
作により触媒を除去し、さらに系を減圧にして溶媒を除
去し、圧力1−20mmHg、温度200−250℃で
蒸留してジシクロヘキシル−2,3,3’,4’−テト
ラカルボン酸エステルを得ることができる。The conditions under which the above-mentioned hydrogenation reaction is carried out vary depending on the catalyst, but usually the hydrogen pressure is several kg / cm 2 -1.
It is preferably 00 kg / cm 2 , especially 20-50 kg / cm 2 , the temperature is 20-200 ° C., particularly 50-150 ° C., and the reaction time is preferably several tens of minutes to 24 hours. Regarding the progress and termination of the hydrogenation reaction,
The determination can be made by obtaining the amount of consumed hydrogen from the pressure gauge. After completion of the reaction, the catalyst was removed from the reaction mixture by a filtration operation, the solvent was removed by reducing the pressure of the system, and dicyclohexyl-2,3,3 ′, distilled at a pressure of 1 to 20 mmHg and a temperature of 200 to 250 ° C. 4'-tetracarboxylic acid ester can be obtained.
【0009】この発明のジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸は、前記のジシクロヘキ
シル−2,3,3’,4’−テトラカルボン酸エステル
を加水分解して得ることができる。前記の加水分解の方
法としては、水中で加熱加水分解、酸加水分解あるいは
アルカリ加水分解とその後の酸析によって行うことがで
きる。前記の酸あるいはアルカリは触媒量であればよ
い。前記の加水分解反応の条件としては、温度が通常2
0−250℃であり、圧力が1−40kg/cm2 であ
り、水の量がジシクロヘキシル−2,3,3’,4’−
テトラカルボン酸エステルの数重量倍−100重量倍程
度であり、反応時間が数10分−24時間程度であるこ
とが好ましい。[0009] The dicyclohexyl-2,3,
3 ′, 4′-Tetracarboxylic acid can be obtained by hydrolyzing the above-mentioned dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid ester. The hydrolysis can be carried out by heating, acid or alkali hydrolysis in water followed by acid precipitation. The acid or alkali may be a catalytic amount. As the conditions for the hydrolysis reaction, the temperature is usually 2
0-250 ° C., pressure 1-40 kg / cm 2 , amount of water is dicyclohexyl-2,3,3 ′, 4′-
It is preferably several times to 100 times the weight of the tetracarboxylic acid ester, and the reaction time is preferably several tens minutes to 24 hours.
【0010】この発明のジシクロヘキシル−2,3,
3’,4’−テトラカルボン酸二無水物は、ジシクロヘ
キシル−2,3,3’,4’−テトラカルボン酸を脱水
閉環させて無水化して得ることができる。前記の無水化
は、常圧−減圧下に不活性ガス流通下に加熱する方法あ
るいは無水酢酸に加熱溶解させて結晶化させる方法によ
って行うことができる。前記の加熱無水化の条件として
は、圧力が1−750mmHgであり、温度が150−
250℃であり、時間が数分−24時間程度であること
が好ましい。ジシクロヘキシル−2,3,3’,4’−
テトラカルボン酸二無水物は、無水化反応と同時に不純
物が昇華されて得ることができる。また、前記の無水酢
酸による無水化は、無水酢酸の量がジシクロヘキシル−
2,3,3’,4’−テトラカルボン酸に対して10倍
モル程度であり、時間が1−3時間程度であり、減圧下
に溶媒および無水酢酸を除去して放冷し、結晶のジシク
ロヘキシル−2,3,3’,4’−テトラカルボン酸二
無水物を得ることができる。[0010] The dicyclohexyl-2,3 of the present invention
3 ′, 4′-Tetracarboxylic dianhydride can be obtained by dehydrating and diclosing dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid to obtain an anhydride. The dehydration can be performed by a method of heating under normal pressure and reduced pressure while flowing an inert gas, or a method of heating and dissolving in acetic anhydride for crystallization. As the conditions for the above-mentioned heat dehydration, the pressure is 1-750 mmHg and the temperature is 150-
It is preferable that the temperature is 250 ° C. and the time is about several minutes to 24 hours. Dicyclohexyl-2,3,3 ', 4'-
The tetracarboxylic dianhydride can be obtained by sublimating impurities simultaneously with the dehydration reaction. In addition, the dehydration with acetic anhydride is performed when the amount of acetic anhydride is dicyclohexyl-
The amount is about 10 times the molar amount of 2,3,3 ', 4'-tetracarboxylic acid, the time is about 1-3 hours, the solvent and acetic anhydride are removed under reduced pressure, and the mixture is left to cool. Dicyclohexyl-2,3,3 ', 4'-tetracarboxylic dianhydride can be obtained.
【0011】[0011]
【実施例】以下、この発明を実施例によって説明する。 実施例1 ジシクロヘキシル−2,3,3’,4’−テトラカルボ
ン酸メチルエステルの製造 攪拌装置の付いた容量1リットルのオ−トクレ−ブに融
点:75℃のビフェニル−2,3,3’,4’−テトラ
カルボン酸メチルエステル〔オルトフタル酸ジメチルエ
ステルを酢酸パラジウムおよび1,10−フェナンソロ
リンの触媒によって酸素存在下、常圧で5−10時間加
熱しカップリング反応させた後、生成したビフェニル−
2,3,3’,4’−テトラカルボン酸メチルエステル
などのアルキルエステルを含む混合物から、触媒を還
元、濾過した後、溶媒を減圧下で除去した後、蒸留およ
びメチルアルコ−ルによる晶析によって製造)77.1
g(0.2モル)、テトラヒドロフラン386gおよび
活性炭に5重量%ロジウムを担持させた触媒(エヌ・イ
−ケムキャット社製)7.7gを仕込み、水素圧力30
kg/cm2 、反応温度100℃で所定量の水素が吸収
されるまで水素化反応を行った。反応後、触媒を濾過操
作により除去した後、エバポレ−タ−により50℃に加
熱して溶媒のテトラヒドロフランを除去し、白色ワック
ス状のジシクロヘキシル−2,3,3’,4’−テトラ
カルボン酸メチルエステル73.0g(0.19モル)
を得た。この白色ワックス状の赤外吸収スペクトル(日
本分光社製JAS.CO FT/IR−5300型赤外
分光光度計を用いKBr法で測定)を第1図に示す。1
H−NMR(日本電子社製GSX−400型 核磁気共
鳴スペクトロメ−タ−)による分析の結果、ベンゼン核
水素および炭素−炭素二重結合に結合した水素は検出さ
れず、水素化反応は完結していることが確認された。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to embodiments. Example 1 Preparation of dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid methyl ester Biphenyl-2,3,3 ′ having a melting point of 75 ° C. was placed in a 1-liter autoclave equipped with a stirrer. 4,4'-tetracarboxylic acid methyl ester [orthophthalic acid dimethyl ester is subjected to a coupling reaction by heating at normal pressure for 5 to 10 hours in the presence of oxygen using a catalyst of palladium acetate and 1,10-phenanthroline to form biphenyl-
From a mixture containing an alkyl ester such as 2,3,3 ', 4'-tetracarboxylic acid methyl ester, the catalyst is reduced and filtered, the solvent is removed under reduced pressure, and distillation and crystallization by methyl alcohol are carried out. 77.1)
g (0.2 mol), 386 g of tetrahydrofuran, and 7.7 g of a catalyst in which 5% by weight of rhodium is supported on activated carbon (manufactured by N-Chemcat), and hydrogen pressure of 30
The hydrogenation reaction was performed at a reaction temperature of 100 ° C./kg/cm 2 until a predetermined amount of hydrogen was absorbed. After the reaction, the catalyst was removed by filtration, followed by heating to 50 ° C. by an evaporator to remove tetrahydrofuran as a solvent, and a white waxy methyl dicyclohexyl-2,3,3 ′, 4′-tetracarboxylate. 73.0 g (0.19 mol) of ester
I got FIG. 1 shows the infrared absorption spectrum of this white wax (measured by the KBr method using a JAS.CO FT / IR-5300 type infrared spectrophotometer manufactured by JASCO Corporation). 1
As a result of analysis by 1 H-NMR (GSX-400 Nuclear Magnetic Resonance Spectrometer manufactured by JEOL Ltd.), benzene nuclear hydrogen and hydrogen bonded to a carbon-carbon double bond were not detected, and the hydrogenation reaction was completed. It was confirmed that.
【0012】実施例2 ジシクロヘキシル−2,3,3’,4’−テトラカルボ
ン酸の製造 攪拌装置の付いた容量1リットルのオ−トクレ−ブにジ
シクロヘキシル−2,3,3’,4’−テトラカルボン
酸メチルエステル40g(0.1モル)、水800gを
仕込み、槽内を窒素で不活性化させた。200℃に加熱
して8時間攪拌し反応させた。反応終了後、反応液をエ
バポレ−タ−により過剰の水を除去し、乾燥させて3
3.2g(0.097モル)の白色粉末状結晶のジシク
ロヘキシル−2,3,3’,4’−テトラカルボン酸を
得た。この結晶の赤外吸収スペクトルを第2図に示す。
1 H−NMRによる分析の結果、9ppmのカルボキシ
ル基プロトンに基づく吸収と0.9−3.0ppmのシ
クロヘキサン環プロトンに基づく吸収の積分強度比は、
4.3:18.1であり、理論値に一致した。また、こ
の白色結晶は融点が118.0−123.5℃であっ
た。Example 2 Production of dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid Dicyclohexyl-2,3,3', 4'- was added to a 1-liter autoclave equipped with a stirrer. 40 g (0.1 mol) of tetracarboxylic acid methyl ester and 800 g of water were charged, and the inside of the tank was inactivated with nitrogen. The mixture was heated to 200 ° C. and stirred for 8 hours to react. After the completion of the reaction, excess water was removed from the reaction solution by an evaporator, and the solution was dried.
3.2 g (0.097 mol) of dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid as white powdery crystals was obtained. FIG. 2 shows the infrared absorption spectrum of this crystal.
As a result of the analysis by 1 H-NMR, the integrated intensity ratio of the absorption based on 9 ppm of the carboxyl group proton and the absorption based on 0.9 to 3.0 ppm of the cyclohexane ring proton is as follows.
4.3: 18.1, which was in agreement with the theoretical value. The melting point of the white crystal was 118.0-123.5 ° C.
【0013】実施例3 ジシクロヘキシル−2,3,3’,4’−テトラカルボ
ン酸二無水物の製造 昇華用の容量1リットルのガラス容器にジシクロヘキシ
ル−2,3,3’,4’−テトラカルボン酸13.7g
(0.04モル)を仕込み、圧力1mmHg、温度20
0℃で10時間無水化反応を行った。冷却後、不純物が
無水化反応と同時に昇華除去された白色結晶を得た。こ
の結晶の赤外吸収スペクトルを第3図に示す。また、1
H−NMRによる分析の結果、9ppmのカルボキシル
基プロトンに基づく吸収はなく、無水物になっているこ
とが確認された。またこの結晶の融点は87.3−9
0.8℃であった。Example 3 Preparation of dicyclohexyl-2,3,3 ', 4'-tetracarboxylic dianhydride Dicyclohexyl-2,3,3', 4'-tetracarboxylic acid was placed in a 1-liter glass container for sublimation. 13.7 g of acid
(0.04 mol), pressure 1 mmHg, temperature 20
The dehydration reaction was performed at 0 ° C. for 10 hours. After cooling, white crystals were obtained in which impurities were sublimated and removed simultaneously with the dehydration reaction. FIG. 3 shows the infrared absorption spectrum of this crystal. Also 1
As a result of analysis by H-NMR, it was confirmed that there was no absorption based on 9 ppm of carboxyl group protons, and the product was an anhydride. The melting point of this crystal was 87.3-9.
0.8 ° C.
【0014】比較例1 実施例1で使用した1リットルのオ−トクレ−ブにビフ
ェニル−2,3,3’,4’−テトラカルボン酸66.
1g(0.2モル)、テトラヒドロフラン386g、お
よび活性炭に5重量%ロジウムを担持させた触媒(エヌ
・イ−ケムキャット社製)6.6gを仕込み、水素圧力
30kg/cm2 、反応温度100℃で5時間攪拌を続
けたが水素の吸収は認められず、水素化反応は進行せず
ジシクロヘキシル−2,3,3’,4’−テトラカルボ
ン酸メチルエステルを得ることができなかった。Comparative Example 1 Biphenyl-2,3,3 ', 4'-tetracarboxylic acid was added to 1 liter of autoclave used in Example 1.
1 g (0.2 mol), 386 g of tetrahydrofuran, and 6.6 g of a catalyst having 5% by weight of rhodium supported on activated carbon (manufactured by N-Chemcat Co.) were charged, and hydrogen pressure was 30 kg / cm 2 and the reaction temperature was 100 ° C. Stirring was continued for 5 hours, but no absorption of hydrogen was recognized, and the hydrogenation reaction did not proceed, and dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid methyl ester could not be obtained.
【0015】比較例2 実施例1で使用した1リットルのオ−トクレ−ブにビフ
ェニル−2,3,3’,4’−テトラカルボン酸二無水
物58.8g(0.2モル)、テトラヒドロフラン38
6g、および活性炭に5重量%ロジウムを担持させた触
媒(エヌ・イ−ケムキャット社製)5.9gを仕込み、
水素圧力30kg/cm2 、反応温度100℃で5時間
攪拌を続けたが水素の吸収は認められず、水素化反応は
進行せずジシクロヘキシル−2,3,3’,4’−テト
ラカルボン酸メチルエステルを得ることができなかっ
た。Comparative Example 2 To 1 liter of autoclave used in Example 1 was added 58.8 g (0.2 mol) of biphenyl-2,3,3 ', 4'-tetracarboxylic dianhydride and tetrahydrofuran. 38
6 g, and 5.9 g of a catalyst having 5% by weight of rhodium supported on activated carbon (manufactured by N-Chemcat Co.) were charged.
Stirring was continued at a hydrogen pressure of 30 kg / cm 2 and a reaction temperature of 100 ° C. for 5 hours, but no absorption of hydrogen was observed, the hydrogenation reaction did not proceed, and methyl dicyclohexyl-2,3,3 ′, 4′-tetracarboxylate was obtained. The ester could not be obtained.
【0016】[0016]
【発明の効果】この発明によれば、ポリマ−原料または
その前駆体である新規なジシクロヘキシル−2,2,
3’,4’−テトラカルボン酸化合物又はその二無水物
を得ることができる。According to the present invention, a novel dicyclohexyl-2,2,2, which is a polymer raw material or a precursor thereof, is obtained.
A 3 ′, 4′-tetracarboxylic acid compound or a dianhydride thereof can be obtained.
【0017】また、この発明によれば、ジシクロヘキシ
ル−2,2,3’,4’−テトラカルボン酸化合物又は
その二無水物を容易に製造することができる。Further, according to the present invention, a dicyclohexyl-2,2,3 ', 4'-tetracarboxylic acid compound or a dianhydride thereof can be easily produced.
【図1】図1は、実施例1で得られたジシクロヘキシル
−2,2,3’,4’−テトラカルボン酸メチルエステ
ルの赤外吸収スペクトル図である。FIG. 1 is an infrared absorption spectrum of dicyclohexyl-2,2,3 ′, 4′-tetracarboxylic acid methyl ester obtained in Example 1.
【図2】図2は、実施例2で得られたジシクロヘキシル
−2,2,3’,4’−テトラカルボン酸の赤外吸収ス
ペクトル図である。FIG. 2 is an infrared absorption spectrum of dicyclohexyl-2,2,3 ′, 4′-tetracarboxylic acid obtained in Example 2.
【図3】図3は、実施例3で得られたジシクロヘキシル
−2,2,3’,4’−テトラカルボン酸二無水物の赤
外吸収スペクトル図である。FIG. 3 is an infrared absorption spectrum of dicyclohexyl-2,2,3 ′, 4′-tetracarboxylic dianhydride obtained in Example 3.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C07C 69/75 C07C 69/75 Z C07D 307/89 C07D 307/89 Z // C07B 61/00 300 C07B 61/00 300 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI C07C 69/75 C07C 69/75 Z C07D 307/89 C07D 307/89 Z // C07B 61/00 300 C07B 61/00 300
Claims (3)
−2,3,3’,4’−テトラカルボン酸化合物。 【化1】 (式中、Xは水素原子、又は炭素数1以上のアルキル基
を示す。)1. A dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic acid compound represented by the following general formula. Embedded image (In the formula, X represents a hydrogen atom or an alkyl group having 1 or more carbon atoms.)
−2,3,3’,4’−テトラカルボン酸二無水物。 【化2】 2. A dicyclohexyl-2,3,3 ′, 4′-tetracarboxylic dianhydride represented by the following general formula. Embedded image
ラカルボン酸エステルを貴金属水素化触媒または貴金属
の坦持触媒などの水素化触媒によって水素化反応させる
工程を含み、必要であればさらに加水分解、無水化処理
する工程を含む請求項1あるいは請求項2に記載のジシ
クロヘキシル−2,2,3’,4’−テトラカルボン酸
化合物又はその二無水物の製造法。3. A step of hydrogenating biphenyl-2,3,3 ′, 4′-tetracarboxylic acid ester with a hydrogenation catalyst such as a noble metal hydrogenation catalyst or a noble metal supported catalyst, if necessary. The method for producing a dicyclohexyl-2,2,3 ', 4'-tetracarboxylic acid compound or a dianhydride thereof according to claim 1 or 2, further comprising a step of performing hydrolysis and dehydration treatment.
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JP29232897A JP3608354B2 (en) | 1997-10-24 | 1997-10-24 | Dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid compound |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002322119A (en) * | 2001-04-25 | 2002-11-08 | Ube Ind Ltd | rac-cis-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydride and their preparation |
JP2002322120A (en) * | 2001-04-25 | 2002-11-08 | Ube Ind Ltd | rac-trans-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydride and their preparation |
JP2011046877A (en) * | 2009-08-28 | 2011-03-10 | Mitsubishi Chemicals Corp | Dicyclohexyl-3, 3', 4, 4'-tetracarboxylic acid dianhydride-containing composition, and polyamic acid and polyimide resin obtained from the same |
CN111032214A (en) * | 2017-09-01 | 2020-04-17 | 恩亿凯嘉股份有限公司 | Catalyst for nuclear hydrogenation |
-
1997
- 1997-10-24 JP JP29232897A patent/JP3608354B2/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002322119A (en) * | 2001-04-25 | 2002-11-08 | Ube Ind Ltd | rac-cis-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydride and their preparation |
JP2002322120A (en) * | 2001-04-25 | 2002-11-08 | Ube Ind Ltd | rac-trans-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydride and their preparation |
JP4543576B2 (en) * | 2001-04-25 | 2010-09-15 | 宇部興産株式会社 | rac-cis-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydrides and process for their preparation |
JP4543575B2 (en) * | 2001-04-25 | 2010-09-15 | 宇部興産株式会社 | rac-trans-dicyclohexyl-3,3 ', 4,4'-tetracarboxylic acid, dianhydrides and process for their preparation |
JP2011046877A (en) * | 2009-08-28 | 2011-03-10 | Mitsubishi Chemicals Corp | Dicyclohexyl-3, 3', 4, 4'-tetracarboxylic acid dianhydride-containing composition, and polyamic acid and polyimide resin obtained from the same |
CN111032214A (en) * | 2017-09-01 | 2020-04-17 | 恩亿凯嘉股份有限公司 | Catalyst for nuclear hydrogenation |
CN111032214B (en) * | 2017-09-01 | 2024-02-06 | 恩亿凯嘉股份有限公司 | Catalyst for nuclear hydrogenation |
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